EP1297220B1 - Verfahren zur papierherstellung mittels faser- und füllstoff-komplexen - Google Patents

Verfahren zur papierherstellung mittels faser- und füllstoff-komplexen Download PDF

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Publication number
EP1297220B1
EP1297220B1 EP01950431A EP01950431A EP1297220B1 EP 1297220 B1 EP1297220 B1 EP 1297220B1 EP 01950431 A EP01950431 A EP 01950431A EP 01950431 A EP01950431 A EP 01950431A EP 1297220 B1 EP1297220 B1 EP 1297220B1
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Prior art keywords
filler
fiber
fines
paper
residue
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EP01950431A
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English (en)
French (fr)
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EP1297220A4 (de
EP1297220A1 (de
Inventor
Alexander A. Koukoulas
Thomas E. Altman
M. C. Matthew
Thomas E. Amidon
Fernand Mora
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International Paper Co
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International Paper Co
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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
    • D21H17/70—Inorganic compounds forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with other substances added separately
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/16—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
    • D21H11/20—Chemically or biochemically modified fibres
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
    • D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/675—Oxides, hydroxides or carbonates

Definitions

  • the present invention relates to a process for loading particulate filler complexes, and more particularly, increasing the deposition and retention of these filler complexes on fibers for manufacture of paper or paperboard products.
  • Inorganic material such as precipitated calcium carbonate (PCC) ground calcium carbonate (GCC), clay and talc are used extensively as fillers in the paper making process. Filler loading levels of 12-25% are typical in current paper making strategy to improve optical properties of the paper such as brightness and opacity. In some instances, the economics of substituting expensive fiber with inexpensive filler lends added incentive.
  • PCC precipitated calcium carbonate
  • GCC ground calcium carbonate
  • talc are used extensively as fillers in the paper making process. Filler loading levels of 12-25% are typical in current paper making strategy to improve optical properties of the paper such as brightness and opacity. In some instances, the economics of substituting expensive fiber with inexpensive filler lends added incentive.
  • retention aids are used. Normally retention aids are long chained polymeric compounds that flocculate the furnish and enhance filler-fiber "attachment.” However, high flocculation levels lead to non-uniformity in the web and poor paper formation.
  • the crystals of precipitated calcium carbonate (PCC) are organized essentially in clusters of granules directly grafted on to the microfibrils without any binders or retention aids such that the crystals trap the microfibrils by reliable and non-labile bonding.
  • Srivatsa et al. describes in situ precipitation on secondary fiber furnish.
  • the Cousin et al. patents describe a batch reaction process
  • Matthew et al. describes a continuous process for forming fiber-filler complexes.
  • the complexing process relies on anionic charges located on the fiber surfaces that act as nucleation sites to anchor the calcium carbonate crystal on to the fiber.
  • the precipitating calcium carbonate physically binds on to the fiber at these sites.
  • more surface area is generated and additional anchoring sites are created on the fiber.
  • the present invention provides for a source of fiber having a high surface area (anchoring sites) without the need for additional refining by obtaining them from process streams within the paper making process.
  • the invention identifies sources of furnish that are suitable for fiber-filler complexes and provides methods to use them to improve the economics of the process and quality of product. It also targets improvements in paper machine operations, downstream processing of paper mill effluents and paper product characteristics.
  • PCT Publication WO 99/42657 published on August 26, 1999 describes a process wherein "white water” from a papermaking operation is separated into two components - “laden water” and “clear water” - each of which component is incorporated, respectively, into separate compositions containing calcium bicarbonate and calcium hydroxide. These two compositions are combined to precipitate calcium carbonate on certain fibers.
  • U.S. Patent No. 5,262,006 to Anderson discloses a process of making paper from pulp stock containing calcium sulfate wherein calcium carbonate is precipitated in situ by the addition of soluble calcium salt and carbon dioxide.
  • U.S. Patent No. 3,639,206 to Spruill discloses a method for treating waste water from an alkaline pulping operation by adding thereto calcium oxide or calcium hydroxide followed by carbon dioxide to form a precipitate which presumably entrains therein the fibrous waste materials in the suspension. The latter is removed from the suspension and ultimately disposed of.
  • EP 0604095 and EP 1052227 concern a processes for the treatment of aqueous suspensions of particular waste material which consists of precipitating an alkaline earth metal carbonate in the aqueous suspension such that the particulate material present in the aqueous suspension to be treated is carried into the alkaline earth metal carbonate precipitate.
  • EP 658606 discloses a process for the aggregation of waste solids in waste water from a paper manufacturing factory in which the waste water recovery system includes at least one step in which an alkaline earth metal carbonate is precipitated in the aqueous suspension constituting the waste water to form a mixed aggregate material.
  • WO 99/03928 published on January 20, 1999 describes a process for precipitating crystals of an insoluble white pigment compound in an aqueous medium containing dispersed particles of fine particulate material and fibers to form a composite pigment material comprising a composite fiber matrix, precipitated pigment crystals and fine particulates dispersed and bonded in the matrix.
  • WO 00/39029 published on July 6, 2000 discloses a process for increasing the solids concentration of a dilute aqueous suspension of a particulate carbonate, especially calcium carbonate, to form a concentrated suspension which is fluid enough to enable it to be pumped and delivered through pipes or hoses but viscous enough to prevent the formation of a sediment of the coarser particles present.
  • An object of the invention is to provide a source of fiber having high surface area without the need for refining.
  • a more specific object of the invention is to separate process streams from various points within the paper making process to obtain primary and/or secondary fines for subsequent treatment to form fiber-filler complexes used in the papermaking process to form paper.
  • a specific object of the invention is to provide paper which has enhanced stiffness properties, enhance filler retention and uniform z- and cross direction filler profiles.
  • a more specific object of the invention is to provide target filler levels in the paper that are at least 5% and preferably higher than 20%.
  • the invention provides a method for manufacture of loaded paper or paperboard products, comprising the steps of separating at least one process stream from the papermaking process, wherein the process stream includes fines. Combining the process stream with long fibers and thickening to form a residue. Treating the residue to form fiber-filler complexes and using the fiber-filler complexes in the papermaking process to form the paper.
  • the process streams used in the invention process can be separated from any point along the papermaking process, including points prior to the paper machine, from the paper machine or after the paper machine.
  • the process streams separated may include primary or secondary fines and depending on the stream separated may further include filler particles.
  • the process stream is combined with long fibers, typically having a length greater than 0.1 mm.
  • the long fibers are from any source and can be natural or synthetic. in alternate embodiments, the long fibers are refined to produce greater fiber surface area.
  • the material is thickened to form a wet residue.
  • This residue is preferably treated with calcium and carbonate ions to effect crystallization of calcium carbonate in situ.
  • the crystals of calcium carbonate bond to the fines, long fibers and/or fillers which may be present in the residue.
  • the crystals of calcium carbonate, CaCO 3 are organized essentially in clusters of granules directly grafted onto the fines, filler and/or fiber present in the residue, without binders or retention aids present at the interface between said crystals of PCC and the fines, filler and/or fiber, so that the majority of said crystals of PCC trap said fines, filler and/or fiber by reliable and non-labile bonding to form the fiber-filler complex.
  • the residue formed is treated with particulate filler material to form the fiber-filler complexes.
  • the particulate filler material used may be selected from the group consisting of inorganic pigments, organic pigments, organic latices and hollow spheres.
  • the pigments are selected from the group consisting of talc, clay, TiO 2 , calcium carbonate, silica based pigments and aluminum based pigments.
  • the resulting paper formed has enhanced stiffness properties, enhanced filler retention and has uniform z- and cross direction filler profiles.
  • a method for manufacture of loaded paper or paperboard products comprising separating at least one process stream from the papermaking process; wherein the process stream includes fines; combining said process stream with long fibers and thickening to form a residue; treating the residue to form fiber-filler complexes; and using said fiber-filler complexes in the papermaking process to form the paper.
  • the invention provides a method for loading of filler material for manufacture of paper or paperboard products, comprising separating at least one process stream from the papermaking process; wherein the process stream includes fines; combining said process stream with long fibers and thickening to form a residue; treating the residue with calcium and carbonate ions to effect crystallization of calcium carbonate in situ to form fiber-filler complexes; and using said fiber-filler complexes in the papermaking process to form the paper.
  • the crystals of calcium carbonate, CaCO 3 (PCC), formed are organized essentially in clusters of granules directly grafted onto the fines, filler and/or fiber present in the residue, without binders or retention aids present at the interface between the crystals of PCC and the fines, filler and/or fiber, so that the majority of the crystals of PCC trap said fines, filler and/or fiber by reliable and non-liabile bonding to form the fiber-filler complexes.
  • PCC calcium carbonate
  • the invention provides an improved process for increasing the deposition and retention of particulate filler complexes on fibers for the manufacture of paper or paperboard products.
  • the fiber-filler complexes of the invention may be formed according to the process and parameters as are described in U.S. Patent Nos. 5,731,080 and 5,824,364 to Cousin et al.; 5,665,205 to Srivatsa et al and 5,679,220 to Matthew et al. which all disclose processes involving in situ attachment of precipitated calcium carbonate (PCC).
  • PCC precipitated calcium carbonate
  • the present invention provides an improvement over these processes which are illustrated in the embodiments shown in Figures 1 and 2.
  • the method of the invention involves utilizing process streams from the paper making process.
  • the process streams may be separated after the screening step 4, or at various points along the paper machine 5.
  • the process streams are passed on to a thickener 6 to form a residue.
  • the process stream separated contains fiber fines and may also contain filler material and retention chemicals.
  • the process stream is combined with the pulp fibers to expand the fiber surface area, and thickened to form a residue.
  • This material is treated to deposit precipitated calcium carbonate (PCC) in situ on the fibers 8.
  • the PCC treatment is done on the thickened white water solids after combination with virgin fibers.
  • the expanded surface area of the fiber fines results in high loading of PCC.
  • a method of obtaining a fiber fines stream is either prior to the refining 1' (primary fines) or after refining (secondary fines) is provided.
  • Process streams, including fiber fines, which are obtained at other stations during the papermaking process are encompassed by the invention method.
  • the process streams are separated by separation procedures, including screening and/or cleaners, although other separation methods may be used and are encompassed by the invention.
  • the process streams, including the fiber fines are separated, they are subject to treatment to produce fiber-filler complexes which are used to produce filler loaded paper or paperboard products.
  • the fiber-filler complexes are formed by the processes described in Cousin et al. and Matthew, by adding lime (CaO) and carbon dioxide gas into the reactor to form precipitated calcium carbonate (PCC).
  • CaO lime
  • carbon dioxide gas e.g., calcium carbonate
  • other particulate filler material such as talc, clay, etc, may be added to the fiber fines and used in the papermaking process to form the paper.
  • Figure 3A illustrates the prior art process as described in the Cousin et al. patents where virgin pulp is refined to produce fines which are then subjected to treatment to cause precipitation of calcium carbonate in situ.
  • the fiber-filler complexes formed are cycled to the papermaking machine to produce a loaded paper.
  • the invention provides enhancement of the fiber surface area of the pulp "starting" material, without the need to refine the virgin pulp fibers, by concentrating process streams, including fines and/or filler, from the papermaking process and combining the thickened residue with virgin pulp fibers.
  • the white water process stream 40 which is a by product of the paper machine and includes "fines and filler", is combined with the long fibers 41, thickened 42 and sent to a reactor 43 for treatment to form a fiber-filler complex slurry.
  • the treated pulp slurry is cycled to the papermaking process to produce a loaded paper.
  • Figure 4 is a more detailed illustration of the process of the invention showing combination of the process stream containing the fiber fines and/or filler 51, with long fibers (virgin pulp) 50.
  • the mixture is then thickened - forming a wet "solid" pad (pulp slurry suspension of 6% solids).
  • the combined mixture of long fibers, fines and filler is essentially the "starting" material for the processes described in the Cousin et al. patents which deposit precipitated calcium carbonate (PCC) in situ on the fibers.
  • the starting fiber material and source of fiber fines can be from virgin, recycled, bleached or unbleached, natural or synthetic pulp.
  • the fiber fines utilized in the invention process can be primary or secondary fines. Typically, primary fines are natural with the pulp and are separated prior to the refining step.
  • Secondary fibers are generally referred to those fines that are made - a source of secondary fiber fines is in the refining step and other processing steps.
  • Nominally refined pulp hardwood, softwood or a blend of papermaking fibers
  • the source of fines could also be from wet or dry broke, recycled through the paper machine, or from recycled paper (pre- or post consumer waste paper).
  • the invention process is a "closed” system that utilizes “process” water and elements within the papermill which minimizes waste, as opposed to utilizing the mill water effluent which is considered industrial waste.
  • the starting material used was pulp (thickened residue) containing both fines and hardwood fiber.
  • the fines include papermaking fines and other ingredients (including filler/mineral particles) that did not get entrapped on the paper web and made its way through the wire of the paper machine.
  • Dilution water and lime were added sequentially into this line, with the ratio of lime to pulp varied to target desired calcium carbonate loadings.
  • the pulp was mixed with (filtered) slaked lime 72 and mill water (fresh cool water) 73 to a consistency of 1.0 to 3.5%. Mixing is conducted in-line.
  • the slurry of pulp, dilution water and lime pass a static mixer 74 where the ingredients are blended. Gaseous carbon dioxide 75 is injected into the line. The slurry entered another static mixer 74 where all the ingredients are blended again. The slurry passes the reactor 77 at temperatures between 15-60°C (60 to 140 °F). The pH of the outlet stream was monitored and controlled in the range of 6.5 to 7 by adjusting the carbon dioxide flow to the reactor. The fiber-filler complex exiting the reactor is stored in a tank and then sent to the paper machine after further dilution to 0.5 to 0.8% consistency.
  • the paper making process generates both primary and secondary fines.
  • the invention provides a process to segregate these fines upstream from the papermaking process/papermachine. Generally, the size of the fines separated are in the range of 0 to 100 ⁇ m.
  • a classifier is used to separate the fines which are collected and then treated in the "fiber-filler complexing" reactor. The complexes are then returned to the furnish and fed to the papermachine headbox or other points in the paper making process to produce the paper.
  • a series of screens are used (to classify the fiber) and refiners are used to refine only the long fiber fraction.
  • Each screen provide a fines-rich stream that would feed into a reactor to form the fiber/filler complexes.
  • a screen placed before the first refiner would separate out the fines from the pulping and bleaching process (primary fines), while screens placed between the refiners or after the last refiner would separate the secondary fines generated in the refining process.
  • a pump could be used to adjust the consistency similar to the POM pump, and screen and refine pulp directly from the last washer or the high density chest, which is at higher consistency than the thick stock. This embodiment would streamline the process by bypassing the high or low density chests.
  • the fiber/filler complexes are preferably formed according to the process conditions and parameters as are described in the Cousin et al and Matthew et al. patents, although other methods of producing such complexes are encompassed by the invention process.
  • the lime and fines slurry can have a consistency as high as 10% but preferably below 5%.
  • the Cousin et al. process describes a batch reaction process and Matthew et al. describes the continuous approach for forming the complexes.
  • Process temperatures can vary between (06-93°C) 33 to 200 °F.
  • the pressure in the reactor can vary between 1 (14.6 psia) and several atmospheres above ambient.
  • the carbon dioxide gas to lime molar ratios can vary between 0.1 to 10, preferably around 1 to 1.5.
  • the reactor/reaction parameters can be controlled and varied to yield complete reaction and optimal crystal growth and morphology.
  • the carbon dioxide gas used in the reaction could be pure or from a source such as flue gas. Also as described in Matthew et al. preacidifying the fines stream prior to lime addition and other step-wise introduction of lime and carbon dioxide gas can be used in the invention process.
  • the starting fiber material and source of fiber fines can be from virgin, recycled, bleached or unbleached, natural or synthetic pulp.
  • the fiber fines utilized in the invention process can be primary or secondary fines. Typically, primary fines are natural with the pulp and are separated prior to the refining step. Secondary fibers are generally referred to those fines that are made - a source of secondary fiber fines is in the refining step and other processing steps.
  • Nominally refined pulp hardwood, softwood or a blend of papermaking fibers
  • the source of fines could also be from wet or dry broke, recycled through the paper machine.
  • the waste fiber fines vary between 0.5 to 4% of the mill's total fiber production. If filler loading is done at the typical level of 1:3 (fiber:filler), the maximum resulting filler level in the sheet is only 12%. Thus, by using white water fines and waste streams alone it may not be possible to displace all the current "conventional" PCC (up to 23%) with filler-fiber complexes.
  • the invention process provides target filler levels in the paper at levels that are at least 5% and preferably higher than 20%.
  • a pulp stream typically contains long and short fibers.
  • Pressure screens can separate the pulp (feed) into long (reject) and short (accept) fiber streams.
  • Pulp fines exist in any fiber stream. Some are just short fiber/fibrils present in the stock. Most others are generated as fiber furnishes pass through cooking and bleaching processes.
  • the refining step generates a significant amount of fines, therefore the pulp can be screened either before or after the refiner. In this example, the pulp was screened upstream from the refiner.
  • Optimum process conditions such as pulp consistency, feed rate, reject/accept split ratios, etc., as well as the hardware, i.e. screen, rotor-configuration, orfice/slot sizes, etc. were determined.
  • Screening refined pulp is preferably used in the invention process for producing the filler-fiber complexes, however, unrefined pulp can be used as well.
  • Bleached, unrefined southern softwood was used.
  • Several combinations of screening baskets, rotors and screen parameter configurations were used and feed, accept (fines) and reject (long fibers) cuts were collected. These were analyzed for fiber length.
  • the raw data was used to calculate the Arithmetic-weighted length, length-weighted length, weight-weighted length, length-weighted fines % and arithmetic-weighted fines % (all of these are standard reporting units for fiber length).
  • Screening Device #1 was a dewatering press; Screening Device #2 were baskets with 0.05" smooth holes; and Screening Device #3 were baskets with 0.018" slotted holes.
  • Table 4 summarizes a comparison of the physical characteristics of the sheets formed using each of-the filler materials above.
  • Parameter GCC 4C C* at 76% loading C* at 66% loading Brightness, ISO 90.5 89.7 92.4 91.7 Opacity, % 88.5 89 89.3 90.5 Bendtsen Porosity, ml/min 1,450 850 1,070 1,040 Tensile , km 2.6 3.1 2.9 3.1 Scott Bond. J/m2 60 128 106 107 Tear, mN.m2/g 850 770 800 800 Burst , KPa.m2/g 1.1 1.8 1.7 1.7 Ash Retention, % 67 79.7 79.7 78.5

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
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Claims (21)

  1. Verfahren zur Herstellung von Papier- oder Pappeprodukten, bei dem
    mindestens ein Prozessstrom aus dem Papierherstellungsprozess abgetrennt wird, wobei der Prozessstrom Feinstteilchen enthält,
    der Prozessstrom mit langen Fasern kombiniert und unter Bildung eines Rückstandes verdickt wird,
    der Rückstand unter Bildung von Faser-Füllstoff-Komplexen behandelt wird und
    die Faser-Füllstoff-Komplexe in einen Papierherstellungsprozess zur Bildung von Papier verwendet werden.
  2. Verfahren nach Anspruch 1, wobei der Prozessstrom ferner Füllstoffe enthält.
  3. Verfahren nach Anspruch 1, wobei die langen Fasern eine Länge von mehr als 0.1 mm aufweisen.
  4. Verfahren nach Anspruch 1, wobei die langen Fasern natürlich oder synthetisch sind.
  5. Verfahren nach Anspruch 1, wobei die langen Fasern verfeinert sind.
  6. Verfahren nach Anspruch 1, wobei der Prozessstrom aus der Papiermaschine stammt.
  7. Verfahren nach Anspruch 1, wobei der Prozessstrom vor der Papiermaschine gewonnen wird.
  8. Verfahren nach Anspruch 1, wobei der Prozessstrom primäre und/oder sekundäre Feinstteilchen enthält.
  9. Verfahren nach Anspruch 1, wobei der Rückstand zur Auskristallisation von Calciumcarbonat mit Calcium- und Carbonat-Ionen behandelt wird.
  10. Verfahren nach Anspruch 9, wobei die Auskristallisation von Calciumcarbonat in situ erfolgt.
  11. Verfahren nach Anspruch 10, wobei die Calciumcarbonat-Kristalle an die in dem Rückstand vorhandenen Feinstteilchen binden.
  12. Verfahren nach Anspruch 10, wobei die Calciumcarbonatkristalle an die in dem Rückstand vorhandenen langen Fasern binden.
  13. Verfahren nach Anspruch 10, wobei die Calciumcarbonat-Kristalle mechanisch an die in dem Rückstand vorhandenen Füllstoffe binden.
  14. Verfahren nach Anspruch 10 oder Anspruch 21, wobei die Calciumcarbonat-Kristalle, CaCO3 (PCC), im wesentlichen in Clustern aus Granalien organisiert sind, die direkt auf die in dem Rückstand vorhandenen Feinstteilchen, Füllstoffe und/oder Fasern gepfropft sind, und zwar ohne an der Grenzfläche zwischen den PCC-Kristallen und den Feinstteilchen, Füllstoffen und/oder Fasern vorhandene Bindemittel oder Rückhaltehilfen, so dass der Hauptteil der PCC-Kristalle die Feinstteilchen, Füllstoffe und/oder Fasern durch zuverlässige und nicht labile Bindung zur Bildung des Faser-Füllstoff-Komplexes einschließen.
  15. Verfahren nach Anspruch 1, wobei der Rückstand zur Bildung der Faser-Füllstoff-Komplexe mit einem teilchenförmigen Füllstoffmaterial behandelt wird.
  16. Verfahren nach Anspruch 15, wobei das teilchenförmige Füllstoffmaterial unter anorganischen Pigmenten, organischen Pigmenten, organischen Gittern und Hohlsphären ausgewählt ist.
  17. Verfahren nach Anspruch 16, wobei die Pigmente unter Talkum, Tonerde, TiO2, Calciumcarbonat, Pigmenten auf Silica-Basis und Pigmenten auf Aluminium-Basis ausgewählt sind.
  18. Verfahren nach Anspruch 1, wobei das Papier verbesserte Steifigkeitseigenschaften hat.
  19. Verfahren nach Anspruch 1, wobei das Papier eine verbesserte Füllstoffzurückhaltung hat.
  20. Verfahren nach Anspruch 1, wobei das Papier gleichförmige Z- und Querschnittsfüllstoffprofile hat.
  21. Verfahren nach Anspruch 1, wobei der Behandlungsschritt umfasst, dass der Rückstand mit Calcium- und Carbonat-lonen zur Auskristallisation von Calciumcarbonat in situ zur Bildung von Faser-Füllstoff-Komplexen behandelt wird.
EP01950431A 2000-06-27 2001-06-25 Verfahren zur papierherstellung mittels faser- und füllstoff-komplexen Expired - Lifetime EP1297220B1 (de)

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US21459300P 2000-06-27 2000-06-27
US214593P 2000-06-27
PCT/US2001/020161 WO2002000999A1 (en) 2000-06-27 2001-06-25 Method to manufacture paper using fiber filler complexes

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EP1297220A1 EP1297220A1 (de) 2003-04-02
EP1297220A4 EP1297220A4 (de) 2004-03-03
EP1297220B1 true EP1297220B1 (de) 2004-10-06

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US (1) US6592712B2 (de)
EP (1) EP1297220B1 (de)
JP (1) JP3846631B2 (de)
AT (1) ATE278838T1 (de)
AU (1) AU2001271424A1 (de)
CA (1) CA2413709C (de)
DE (1) DE60106253T2 (de)
WO (1) WO2002000999A1 (de)

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US6592712B2 (en) 2003-07-15
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US20020096272A1 (en) 2002-07-25
EP1297220A4 (de) 2004-03-03
JP3846631B2 (ja) 2006-11-15
DE60106253D1 (de) 2004-11-11
CA2413709A1 (en) 2002-01-03
CA2413709C (en) 2006-02-07
EP1297220A1 (de) 2003-04-02
ATE278838T1 (de) 2004-10-15
AU2001271424A1 (en) 2002-01-08
WO2002000999A1 (en) 2002-01-03

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